|Publication number||US7614302 B2|
|Application number||US 11/638,893|
|Publication date||Nov 10, 2009|
|Priority date||Aug 1, 2005|
|Also published as||US20070129901, WO2008076909A2, WO2008076909A3, WO2008077142A2, WO2008077142A3|
|Publication number||11638893, 638893, US 7614302 B2, US 7614302B2, US-B2-7614302, US7614302 B2, US7614302B2|
|Inventors||Rocco DiFoggio, Paul A. Bergren, Jun Han|
|Original Assignee||Baker Hughes Incorporated|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (104), Non-Patent Citations (5), Referenced by (10), Classifications (13), Legal Events (2)|
|External Links: USPTO, USPTO Assignment, Espacenet|
This application is a continuation-in-part of U.S. application Ser. No. 11/194,365 filed Aug. 1, 2005 now U.S. Pat. No. 7,523,640, the full disclosure of which is hereby incorporated by reference herein.
1. Field of the Invention
The invention relates to wellbore evaluation operations. More specifically, the present invention relates to an apparatus and method for ascertaining the compressibility of connate fluid within a wellbore and the presence of a gaseous phase in that fluid.
2. Description of Related Art
The sampling of connate fluid contained in subterranean formations provides a method of testing formation zones of possible interest with regard to hydrocarbon bearing potential. This involves recovering a sample of any formation fluids present for later analysis in a laboratory environment while causing a minimum of damage to the tested formations. The formation sample is essentially a point test of the possible productivity of subsurface earth formations. Additionally, a continuous record of the control and sequence of events during the test is made at the surface. From this record, valuable formation pressure and permeability data as well as data determinative of fluid compressibility, density and viscosity can be obtained for formation reservoir analysis.
Generally connate fluid sampling involves disposing a sonde 10 into a wellbore 5 via a wireline 8. Oppositely located on the outer portion of the sonde 10 usually are a sample port 14 and an urging means 12. When the sample port 14 is proximate to a formation of interest 6, the urging means 12 is extended against the inner surface of the wellbore 5 thereby engaging the sample port 14 into the formation 6. The engagement of the sample port 14 pierces the outer diameter of the wellbore 5 and enables fluid communication between the connate fluid in the formation 6 and the sample port 14. After urging the sample port 14 into the formation 6, the connate fluid can be siphoned into the sonde 10 with a pumping means disposed therein.
Downhole multi-tester instruments have been developed with extendable sampling probes that engage the borehole wall and withdraw fluid samples from a formation of interest as well as measure pressure of the fluid within the formation. Traditionally these downhole instruments comprise an internal draw-down piston that is reciprocated hydraulically or electrically for drawing connate fluid from the formation to the instrument.
Generally, the downhole multi-test sampling devices incorporate a fluid circuit for the sampling system which requires the connate fluid extracted from the formation, together with any foreign matter such as fine sand, rocks, mud-cake, etc. encountered by the sampling probe, to be drawn into a relatively small volume chamber and which is discharged into the borehole when the tool is closed. An example of such a device can be found in U.S. Pat. No. 4,416,152. Before closing, a sample can be allowed to flow into a sample tank through a separate but parallel circuit. Other methods provide for the sample to be collected through the same fluid circuit.
When exposed to an open hole, the fluid characteristics of formation fluid can change rapidly, thus it is important that the formation fluid be removed as quickly as possible. However, it is important that the formation flow rate be regulated in order to prevent dropping the fluid pressure below its “bubble-point” since measuring separated fluids does not result in a representative sample. After having these components come out of solution, they typically cannot be easily recombined which results in an unrepresentative sample having altered fluid properties.
Recently developed reservoir testing devices illustrate one method of measuring the bubble-point pressures of the connate fluid at the time of sample collection. This can be accomplished using known techniques of light transmissibility to detect bubbles in the liquid. However this method has some drawbacks when particulate matter is present in the fluid thereby resulting in possible erroneous results. Other methods include trapping a known volume of formation fluid and increasing its volume gradually at a constant temperature. The measured changes in volume and pressure provide a plot of pressure versus volume in order to ascertain the value of the bubble-point. This value is estimated within the region of the plot where the pressure change with volume first deviates from the initial straight line.
Unfortunately the pumping devices currently in use with the above described sampling devices have some inherent drawbacks. For example, control of the electrical or hydraulic actuation means of the presently used pumping systems is not accurate that in turn results in an inability to fully control the speed of the pumps. Not being able to fully control pump speed prohibits the capability of ceasing pumping operations should the pressure of the connate fluid fall below its bubble point and also hinders the ability to accurately measure the bubble point. Since sampling connate fluid at pressures below its bubble point negatively affects the accuracy of the sampling data results. Therefore a need exists for a means of accurately analyzing properties of connate fluid without affecting the condition or state of the fluid.
The present invention includes a method of analyzing acoustic data comprising, inducing an acoustic signal into a fluid, wherein the fluid is in contact with a first and a second reflective interface, recording data representative of acoustic signals over time as they are reflecting from the interfaces, determining a smoothed first derivative with respect to time of the cumulative sum of squares (CSS) of the filtered data, and cross correlating time-shifted versions of the first derivative with itself. Using this method, the time difference associated with the maximum cross correlation may be found, which is the approximate acoustic travel time.
Optionally, the method may further include performing digital frequency filtering of the raw signal and squaring the filtered amplitude signal; this can create a curve proportional to the acoustic energy at each recorded time. The method may further comprise squaring the raw data, taking the cumulative sum of squares (CSS) of the raw amplitude data, and taking a smoothed second or third derivative of the CSS. A local maximum may be obtained by the second derivative.
Occasionally, the maximum cross correlation value is only slightly larger than the next largest cross correlation value and the correct pulse to use is the one associated with the second largest cross correlation value. This can happen when there is a neighboring acoustic pulse, which has approximately the same peak height as the correct pulse but a different pulse width. Therefore, a further step of thresholding may be used to select the correct pulse for the initial estimate of arrival time. This thresholding may include comparing the value of a first local maximum with the value of a second local maximum. A downhole system may be employed for carrying out the above described methods.
The method disclosed herein provides a method of acoustically evaluating a fluid sample. The evaluation results comprise fluid sound speed, fluid density, fluid thermal conductivity, and from the change in sound speed with pressure near reservoir pressure, the fluid's equation of state as described in U.S. patent application Ser. No. 11/393,770 filed Mar. 30, 2006. With reference now to
As shown, the container 20 should be capable of retaining and storing the fluid 18 within its confines during analysis. Although shown as open at its top, the container 20 can also be sealed thereby fully encapsulating the fluid 18 therein. The signal generator 16 can be attached to the outer or first wall 24 of the container 20 or maintained in place. As will be described herein below, for the purposes of reference, both the first and second surfaces (24, 26) shown adjacent to the signal generator 16 are shown as well as the third and fourth surfaces (28, 30) distal from the signal generator 16.
With respect to the signal generator 16, it can be comprised of any device capable of producing an acoustic signal passable through the fluid. This includes traditional acoustic devices such as piezoelectric devices, however other acoustic transducers can also be used to accomplish this function. For example, an Electro-Magnetic Acoustic Transducer (EMAT) can insert ultrasonic waves into metal by electromagnetic coupling. Alternatively, a pulsed laser that strikes an object can generate acoustic waves at a frequency that depends on the laser pulse frequency. Moreover, the signal generator 16 can also be used as a receiver for receiving and recording reflections of the signals generated by the signal generator 16. A flexural mechanical resonator may be coupled for use with the device disclosed herein, an example of a flexural mechanical resonator is described in detail in U.S. Pat. No. 6,938,470 issued Sep. 6, 2005 ('470 patent), the disclosure of which is incorporated for reference herein in its entirety.
In one alternative of the present device, the sampling system 22 is used with the downhole tool 54 of
In one non-limiting example of operation of the present method disclosed herein, after the sampled fluid is delivered to the sampling system 22, the signal generator 16 might be activated for generation of a signal 17 that is emitted into the sampled fluid. Examples of a signal 17 include one or more acoustic pulses. For the purposes of convenience the generated signal 17 is illustrated as a series of curved lines emanating from the transducer 16. After leaving the signal generator 16, the signal 17 passes through the first and second surfaces (24, 26) of the container 20, into the contained fluid 18, and onto the distal third and fourth surfaces (28, 30). A portion of the generated signal 17 (the reflected signal 19) reflects back to the direction of the signal generator 16. Similarly, the reflected signal 19 is illustrated for convenience as a series of curved lines directed towards the signal generator 16. In the embodiment of
When the signal generator comprises a piezoelectric transducer, a short voltage spike can be applied to the transducer that typically lasts about 1-2 microseconds. This spike causes the transducer to resonate at its resonant frequency, which is typically from about 5 MHz to about 10 MHz. Analogous to a bell that rings for a while after it has been struck by a hammer, the transducer rings, primarily at its resonant frequency, for about a microsecond. An ever-decreasing portion of this microsecond-long pulse bounces back and forth between the tube wall that is bounded by surface 24 and surface 26, (which is in contact with the transducer 16) because a portion of the pulse is transmitted into the fluid 18 upon each bounce off of the surface 26. The transmitted portion of the pulse passes beyond surface 26, enters the fluid 18, reflects from the surface 28, and eventually returns to be detected by the transducer 16. The acoustic transducer serves both as source and receiver. A high-speed (40-70 MHz) analog-to-digital converter may be used for monitoring the signal received by the transducer.
As shown, the signal generator 16 receives and records the reflected signal for subsequent analysis. The recorded signal can either be immediately processed to determine fluid data, transmitted from the downhole tool 54 to a separate site for storage or data processing, or can be recorded within the downhole tool 54 for later analysis.
As is known, the sound speed, c, of a fluid is determined by dividing the travel time of the signal through the fluid 18 by the distance the signal traveled through the fluid. This can be accomplished by designating the letter “d” as the distance between surface 26 and 28. Moreover, the variable 2t can be designated as the time difference between the arrival time of the first echo (corresponding to one round trip going from surface 24 to 26 and back again to 24) and the arrival time of the echo off surface 28 (corresponding to one round trip from 24, past 26, to 28, and eventually, back to 24). Therefore, 2t is amount of time that transpired for sound to travel a round-trip distance (2d) within the fluid 18 from surface 26 to surface 28 and back to surface 26. The sound speed therefore is 2d/2t.
Fluid density can be determined acoustically from the following relationship for an acoustic pulse bouncing back and forth between surface 24 and surface 26:
ρF=ρW(c W /c F)[1+Sqrt(R WF)]/[(1−Sqrt(R WF)]; (1)
ρW=Transducer wall density in g/cc,
ρT=Transducer density in g/cc
cW=Tube wall longitudinal sound speed,
cT=Transducer longitudinal sound speed
ρF=Fluid density in g/cc,
cF=Fluid sound speed,
RWF=Fraction of energy reflected at all/Fluid interface, and
The details of acoustically determining fluid density can be found in pending U.S. Pat. No. 7,024,917 issued Apr. 11, 2006 ('917 patent), the entirety of which is incorporated for reference herein. Fluid density could also be measured by using flexural mechanical resonators as described in the '470 patent. Fluid density could also be determined by any other means such as by measuring the pore pressure gradient across the zone from which the fluid is being extracted. Knowing the fluid's density and measuring its sound speed allows determination of the fluid's compressibility, which is much simpler than the current method of determining compressibility downhole by trapping a volume of fluid, expanding the volume, and measuring the drop in pressure per volume increase.
The bulk modulus B of a fluid is equal to the reciprocal of the compressibility of the fluid, B=1/K. It is also known that the sound speed is equal to the square root of the fluid's bulk modulus divided by the fluid density, c=(B/ρ)1/2. Substituting the reciprocal of compressibility for the bulk modulus and isolating compressibility yields the following equation:
K=1/(c 2ρ) (2)
Accordingly, having determined the fluid density, ρ, and the fluid sound speed, c, as described herein, the fluid compressibility can then be calculated using equation (2).
In one embodiment of the method and apparatus herein disclosed, the raw amplitude data can be digitally frequency filtered. One example of digitally frequency filtered comprises applying a digital bandpass filter to reject any frequencies that are not close to the acoustic source frequency. For example, for a 10 MHz acoustic source and a 40 MHz sampling frequency, the raw data could be processed through a 9-11 MHz digital bandpass filter. Next, the square of the amplitude at each sampling time can be computed. This squared value corresponds to the energy received at that time.
A cumulative sum of squared values (CSS) may then be generated. The CSS represents the cumulative sum of energy received up until that time. The digital bandpass filtering and cumulative sum of squares have already smoothed the raw data and removed some noise. However further data smoothing may still be undertaken of the already filtered cumulative sum of squares data. The further smoothing may comprise taking the first and second numerical derivatives of the CSS. One derivative method includes using the Savitzky-Golay method (Savitzky and Golay, Analytical Chemistry, Vol. 36, No. 8, July 1964), which is based on fitting a polynomial to the curve and computing the derivatives of this polynomial.
Taking the cumulative sum of squares is equivalent to integration and noise averaging (smoothing); a plot of energy pulses is recovered by differentiating this integral. A benefit of integrating followed by differentiation is retention of the smoothing effects of integration and of smoothed numerical differentiation (such as that obtained by using a fitting polynomial in Savitzky-Golay techniques). That is, the smoothed first derivative of the CSS produces a series of smooth peaks representing pulses (packets) of acoustic energy (such as the following peaks of FIG. 4—35, 36, 37, 39, 40, 41 or 65, 67, 69, etc.). Once the approximate travel time has been determined, focus is given to an energy pulse (such as 39 or 72), which occurs later than the initial energy pulse reflection (such as 35 or 65) by the estimated amount of travel time, an improved measurement of travel time can be determined by using the time difference between pinnacles of these peaks (such as pinnacles of peaks 35 versus 39 or of 65 versus 72) instead of simply using the time difference estimated obtained from the cross correlation maximum.
With reference now to
As noted above, the data smoothing is further accomplished by computing the first derivative with respect to time of the cumulative sum of squares; and optionally, the Savitzky-Golay method may be implemented for taking a smoothed numerical derivative. Greater high frequency attenuation may be accomplished by using Savitzky-Golay coefficients of lower order (such as square or cube) polynomials over a fairly large number of points (25 channels). The first derivative of the cumulative sum of squares is the smoothed energy received versus time, which shows distinct acoustic energy pulses. The resulting values produced by the Savitzky-Golay method are shown plotted in the smooth energy data plot 34 of
The presence of signals not generated by the transducer 16 can result in a signal peak, such as the noise peaks (81, 83), being mistakenly chosen as the return signal. Thus a method can be employed to ensure proper identification of the return signals. A method of cross correlation can be used to properly identify the set of peaks 72 representing the reverberations from the third surface 28. One example of cross correlation comprises a mathematical algorithm that slides the first set of peaks along the abscissa proximate to the region where the second set of peaks is expected. The respective ordinate values of the signals are then multiplied at that point; the first peak values are then moved along the abscissa some finite amount to an adjacent point, and multiplied again. The first peaks are moved along at these finite amounts over a set interval and the point where the ordinate values are at a maximum identifies the value of the second set of peaks. Thus in an embodiment herein described, cross correlation is performed on the smoothed first derivative data.
The cross correlation process may include an additional optional step of thresholding, wherein the amplitude values of adjacent peaks are compared to ensure a chosen peak is the first peak of a signal series, which usually consists of a triplet of reverberations (such as 35, 36, and 37 or 39, 40, and 41). In this process the amplitude (or ordinate value) of a peak is compared to the next amplitude of the next adjacent peak in the direction towards the origin (i.e. to the left of the peak under consideration). If the ordinate value of the left peak exceeds 70% of the peak under consideration, the left peak is then chosen as the first signal peak and the process is continued. The process is terminated when the ordinate value of the left peak is less than 70% of the peak under consideration.
To obtain a more accurate travel time, the pinnacle of each pulse can be used as the arrival time of that pulse. At the pinnacle, the slope of the energy pulse (the second derivative of the CSS) becomes zero. The acoustic signal over time is collected at evenly spaced time steps. To improve sound speed resolution, interpolation between time steps is performed. Focus is then given to the pair of neighboring time steps (located on either side of a peak's pinnacle such as time steps 78 and 79) for which the second derivative of the CSS has opposite signs. The time at which the second derivative crosses zero is estimated by interpolating between these time steps (78, 79). The sign of the third derivative of the CSS is one way to determine whether a point at which the second derivative of CSS becomes zero represents the pinnacle of a peak (a downward negative curvature) or the lowest point of a valley (an upward positive curvature). Interpolation improves the sound speed resolution by approximately a factor of ten compared to simply rounding to the nearest time step.
In order to determine the local maxima and minima of the first derivative, the second derivative is taken of the cumulative sum of squares using Savitzky-Golay coefficients of a low order and a large number of points. A local maxima (pulse energy peak) from the first derivative curve can be used to obtain a more precise value of the time at which a particular pulse reflection is received by the transducer 16. It should be pointed out that the second derivative crosses zero when the first derivative reaches either its local maxima or local minima. A pulse peak occurs between two channels (78, 79) whenever the second derivative changes from positive (in the left channel 78) to negative (in the right channel 79) with increasing time. Sub-channel time resolution can be achieved by interpolating so as to estimate the location between two channels where the second derivative crosses zero. Alternatively, energy maxima can be distinguished from energy minima (both of which correspond to zeros of the second derivative of the CSS) based on the sign of the third derivative of the CSS.
Using the data obtained from the processed signal, the sound speed of the fluid within the vessel 20 is twice the wall thickness divided by the (round-trip) time between reverberation pulse peaks within the tube wall. The wall sound speed may change with temperature or with pressure of the fluid inside the tube thus causing the wall's acoustic impedance to change. The wall's acoustic impedance must be known to compute fluid density from fluid sound speed and the decay rate of within-wall pulse echo reverberations. Direct downhole measurement of the wall's sound speed can be made from the wall thickness and the time between within-wall pulse peak reverberations. The wall speed is one parameter used to calculate the density of whatever fluid is in contact with the wall. Another factor in calculating fluid density is the wall density but changes in the wall's density with temperature and pressure are a much smaller effect that can usually be ignored or estimated from a table.
The smooth data plot 34 comprises reflected signals both from signal reverberations within the near wall 25 (between the first and second surfaces 24 and 26) as well as a reflection from the far wall 29 (third surface 28). The near wall reflected signals are illustrated as curves (35, 36, 37) on the smooth data plot 34. The far wall reflected signals are also illustrated as curves (39, 40, 41) on the smooth data plot 34. The acoustic signal reverberating within the near wall decays over time, this can be seen in the decreasing local maxima of the curves (35, 36, 37) of the smooth data plot 34 of
The downhole tool 54 may be part of a downhole measurement system, wherein the system samples downhole fluid, conducts acoustic tests on the fluid to obtain raw data, and processes the data. The data processing can include the smoothing and the taking of derivatives described above. The measurement system can also include an analyzer that is configured to carry out all or a portion of the above described data processing steps. The analyzer may comprise an information handling system 84. Where the information handling system 84 can be included within the downhole tool 54 or at the surface. When at the surface the information handling system 84 can, as represented by the double-headed arrow, be in constant communication with the downhole tool 54 to receive data, or can be later connected for subsequent data communication. The information handling system 84 may include a processor, memory accessible by the processor, nonvolatile storage area accessible by the processor, and logics for performing each of the steps above described.
The present invention described herein, therefore, is well adapted to carry out the objects and attain the ends and advantages mentioned, as well as others inherent therein. While a presently preferred embodiment of the invention has been given for purposes of disclosure, numerous changes exist in the details of procedures for accomplishing the desired results. For example, production of the generated signal 17 is not limited to a signal generator 16 disposed within or adjacent to the sampling system 22, but could include signal generators from remote sources. The remote signal sources could be from ballistics, geophones, airguns, or any other known signal-generating source. Additionally, the raw data smoothed and processed in accordance with the methods herein described is not limited to the sampling system of
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|U.S. Classification||73/597, 73/602|
|International Classification||G01N29/50, G01N29/04|
|Cooperative Classification||G01N29/024, G01N29/222, G01N2291/02433, E21B49/10, G01N29/032|
|European Classification||G01N29/024, G01N29/032, E21B49/10, G01N29/22F|
|Feb 5, 2007||AS||Assignment|
Owner name: BAKER HUGHES INCORPORATED, TEXAS
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:DIFOGGIO, ROCCO;BERGREN, PAUL;HAN, JUN;REEL/FRAME:018856/0399;SIGNING DATES FROM 20070125 TO 20070129
|Mar 7, 2013||FPAY||Fee payment|
Year of fee payment: 4